WO2008057240A9 - Anticorps anti-htnfalpha cristallisés - Google Patents

Anticorps anti-htnfalpha cristallisés

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Publication number
WO2008057240A9
WO2008057240A9 PCT/US2007/022622 US2007022622W WO2008057240A9 WO 2008057240 A9 WO2008057240 A9 WO 2008057240A9 US 2007022622 W US2007022622 W US 2007022622W WO 2008057240 A9 WO2008057240 A9 WO 2008057240A9
Authority
WO
WIPO (PCT)
Prior art keywords
antibody
crystals
crystallization
around
buffer
Prior art date
Application number
PCT/US2007/022622
Other languages
English (en)
Other versions
WO2008057240A2 (fr
WO2008057240A3 (fr
Inventor
David W Borhani
Wolfgang Fraunhofer
Hans-Juergen Krause
Anette Koenigsdorfer
Gerhard Winter
Stefan Gottschalk
Original Assignee
Abbott Biotech Ltd
David W Borhani
Wolfgang Fraunhofer
Hans-Juergen Krause
Anette Koenigsdorfer
Gerhard Winter
Stefan Gottschalk
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=39364990&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2008057240(A9) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to EP07852953.4A priority Critical patent/EP2089428B1/fr
Priority to KR1020147033811A priority patent/KR20150002896A/ko
Priority to AU2007318120A priority patent/AU2007318120B2/en
Priority to MX2009004351A priority patent/MX2009004351A/es
Priority to CA002667655A priority patent/CA2667655A1/fr
Priority to JP2009534651A priority patent/JP2010507670A/ja
Priority to NZ576133A priority patent/NZ576133A/xx
Application filed by Abbott Biotech Ltd, David W Borhani, Wolfgang Fraunhofer, Hans-Juergen Krause, Anette Koenigsdorfer, Gerhard Winter, Stefan Gottschalk filed Critical Abbott Biotech Ltd
Priority to RU2009119988/10A priority patent/RU2486296C2/ru
Priority to ES07852953.4T priority patent/ES2442258T3/es
Priority to BRPI0717335-0A2A priority patent/BRPI0717335A2/pt
Publication of WO2008057240A2 publication Critical patent/WO2008057240A2/fr
Publication of WO2008057240A9 publication Critical patent/WO2008057240A9/fr
Publication of WO2008057240A3 publication Critical patent/WO2008057240A3/fr
Priority to IL198223A priority patent/IL198223A/en
Priority to HK09109260.5A priority patent/HK1129400A1/xx

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
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    • C07K16/00—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies
    • C07K16/18—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans
    • C07K16/24—Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies against material from animals or humans against cytokines, lymphokines or interferons
    • C07K16/241—Tumor Necrosis Factors
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    • A61K39/395—Antibodies; Immunoglobulins; Immune serum, e.g. antilymphocytic serum
    • A61K39/39533—Antibodies; Immunoglobulins; Immune serum, e.g. antilymphocytic serum against materials from animals
    • A61K39/3955—Antibodies; Immunoglobulins; Immune serum, e.g. antilymphocytic serum against materials from animals against proteinaceous materials, e.g. enzymes, hormones, lymphokines
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    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
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Definitions

  • the present invention relates to a batch crystallization method for crystallizing an anti- hTNFalpha antibody which allows the production of said antibody on an industrial scale; antibody crystals as obtained according to said method; compositions containing said crystals as well as methods of use of said crystals and compositions.
  • immunoglobulin crystals have been known for a long time.
  • the first example of immunoglobulin crystals were described 150 years ago by an English physician, Henry Bence Jones; he isolated crystals of an abnormal Ig light chain dimer from the urine of a myeloma patient (Jones 1848). Such abnormal lgs have been known ever since as Bence Jones proteins.
  • the spontaneous crystallization of a distinct abnormal Ig from the serum of a myeloma patient was described (von Bons- dorf, Groth et al. 1938), apparently an Ig heavy chain oligomer (MW 200 kDa).
  • trastuzumab Herceptin®
  • Crystalline trastuzumab suspensions were therapeutically efficacious in a mouse tumor model, thus demonstrating retention of biological activity by crystalline trastuzumab (Yang, Shenoy et al. 2003).
  • McPherson pro- vides extensive details on tactics, strategies, reagents, and devices for the crystallization of macromolecules. He does not, however, provide a method to ensure that any given macromolecule can indeed be crystallized by a skilled person with reasonable expectation of success. McPherson states for example : "Whatever the procedure, no effort must be spared in refining and optimizing the parameters of the system, both solvent and solute, to encourage and promote specific bonding interactions between molecules and to stabilize them once they have formed. This latter aspect of the problem generally depends on the specific chemical and physical properties of the particular protein or nucleic acid being crystallized.” (McPherson 1999, p. 159)
  • Baldock et al (1996) reported on a comparison of microbatch and vapor diffusion for initial screening of crystallization conditions.
  • Six commercially available proteins were screened using a set of crystallization solutions. The screens were performed using the most common vapor diffusion method and three variants of a microbatch crystalli- zation method, including a novel evaporation technique. Out of 58 crystallization conditions identified, 43 (74%) were identified by microbatch, while 41 (71 %) were identified by vapor diffusion. Twenty-six conditions were found by both methods, and 17 (29%) would have been missed if microbatch had not been used at all. This shows that the vapor diffusion technique, which is most commonly used in initial crystallization screens does not guarantee positive results.
  • Human TNFalpha (hTNFalpha) is considered as a causative agent of numerous dis- eases. There is, therefore, a great need for suitable methods of treating such hTNFalpha related disorders.
  • One promising therapeutic approach comprises the administration of pharmaceutically effective doses of anti-human TNFalpha antibodies.
  • D2E7 or generically adalimumab, has been put on the market and is commercialised under the trade name HUMI RA®.
  • WO-A-02/072636 disclosed the crystallization of the whole, intact antibodies Rituximab, Infliximab and Trastuzumab. Most of the crystallization experiments were performed with chemicals with unclear toxicity, like imidazole, 2-cyclohexyl-ethanesulfonate (CHES), methylpentanediol, copper sulphate, and 2-morpholino-ethanesulfonate (MES). Most of the examples used seed crystals to initiate crystallization.
  • CHES 2-cyclohexyl-ethanesulfonate
  • MES 2-morpholino-ethanesulfonate
  • WO-A-2004/009776 disclosed crystallization experiments in the microliter scale using the sitting drop vapor diffusion technique by mixing equal volumes (1 ⁇ l) of different crystallization buffers and D2E7 F(ab)' 2 or Fab fragments. While several experimental conditions were reported for each of said fragments, no successful crystallization of the whole, intact D2E7 antibody was reported.
  • the problem to be solved according to the present invention is, therefore, to develop suitable batch crystallization conditions for anti-hTNFalpha antibodies, in particular for the human anti-hTNFalpha antibody D2E7, and to establish crystallization process conditions applicable to volumes relevant for industrial antibody crystal production. At the same time a crystallization process should be established that does not make use of toxic agents, which might negatively affect the pharmaceutical applicability of such antibodies.
  • the above-mentioned problem was, surprisingly, solved by the finding that it is possible to obtain crystals of a whole anti-hTNFalpha antibody in batch crystallization volumes above the microliter scale by applying physiologically acceptable inorganic phosphate salts as the crystallization-inducing agent.
  • the invention in a first aspect relates to a batch crystallization method for crystallizing an anti-hTNFalpha antibody, comprising the steps of: a) providing an aqueous solution of said antibody in admixture with an inorganic phosphate salt as crystallization agent, as for example by mixing an aqueous solution of said antibody, wherein the antibody preferably is present in dissolved form, with an aqueous crystallization solution comprising an inorganic phosphate salt as crystallization agent in dissolved form, or alternatively by adding said crystallization agent in solid form; and b) incubating said aqueous crystallization mixture until crystals of said antibody are formed.
  • the crystallization method of the invention generally is performed at a pH of said aqueous crystallization mixture in the range of about pH 3 to about 5, in particular about 3.5 to about 4.5, or about 3.7 to about 4.2.
  • said aqueous crystallization mixture may contain at least one buffer.
  • Said buffer may, in particular, comprise an acetate component as main component, especially an alkali metal salt, in particular, sodium acetate.
  • Said salt is adjusted by addition of an acid, in particular acetic acid, to the required pH.
  • the buffer concentration (total acetate) in said aqueous crys- tallization mixture is 0 to about 0.5 M, or about 0.02 to about 0.5 M, as for example about 0.05 to about 0.3 M, or about 0.15 to about 0.2 M.
  • the phosphate salt used as the precipitating agent is selected from hydrogen- phosphate salts, such as mono- or dihydrogenphosphate salts, in particular an ammonium salt or an alkali metal salt, for example a salt containing Na + or K + ions, or a mixture thereof comprising of at least two different salts.
  • hydrogen- phosphate salts such as mono- or dihydrogenphosphate salts, in particular an ammonium salt or an alkali metal salt, for example a salt containing Na + or K + ions, or a mixture thereof comprising of at least two different salts.
  • Suitable examples are: NaH 2 PO 4 , Na 2 HPO 4 , KH 2 PO 4 , K 2 HPO 4 , NH 4 H 2 PO 4 , (NH 4 J 2 HPO 4 , and mixtures thereof.
  • the phosphate salt concentration in the crystallization mixture is in the range of about 1 to about 6 M, for example a range of about 1.0 to about 4.0 M, or about 1.0 to about 3.0 M, or about 1.5 to about 2.8 M, or about 2.0 to about 2.6M.
  • protein solution and crystallization solution are combined in a ratio of about 1 :1.
  • molarities of the buffering agents / crystallization agents in the original crystallization solution are about double as high as in the crystallization mixture.
  • the crystallization method is performed in a batch volume in the range of about 1 ml to about 20000 I, or 1 ml to about 15000 I, or 1 ml to about 12000 I, or about 1 ml to about 10000 I 1 or 1 ml to about 6000 I 1 or 1 ml to about 3000 I 1 or 1 ml to about 1000 I, or 1 ml to about 100 I 1 as for example about 50 ml to about 8000 ml, or about 100 ml to about 5000 ml, or about 1000 ml to about 3000 ml; or about 1 I to about 1000 I; or about 10 I to about 500 I.
  • the crystallization method of the invention may be performed so that at least one of the following additional crystallization conditions is achieved: a) incubation is performed for between about 1 hour to about 60 days, for example about 1 to about 30 days, or about 2 to 10 days; b) incubation is performed at a temperature between about 0 0 C and about 50 0 C, for example about 4 0 C and about 37 0 C; c) the antibody concentration (i.e. protein concentration) in the crystallization mixture is in the range of about 1 to 200 mg/ml or 1 to 100 mg/ml, for example 1.5 to 20 mg/ml, in particular in the range of about 2 to 15 mg/ml, or 5 to 10 mg/ml.
  • the protein concentration may be determined according to standard procedures for protein determination.
  • crystallization is performed under the following conditions of the crystallization mixture:
  • Phosphate salt NaH 2 PO 4 , 1.5 to 2.5 M buffer: total acetate, 0 to 0.3 M pH: 3.6 to 4.2 anti-hTNFalpha concentration: 3 to 10 mg/ml Temperature: 18 to 24 0 C
  • crystallization mixtures as outlined above are usually obtained by adding a crystallization agent in solution or as solid to the protein solution. Both solutions may be, but do not have to be buffered. Crystallization agent molarity and buffer molarity in the original crystallization solution is usually higher than in the crystallization mixture as it is "diluted" with the protein solution.
  • the crystallization method of the invention may further comprise the step of drying the obtained crystals. Suitable drying methods comprise evaporative drying, spray drying, lyophilization, vacuum drying, fluid bed drying, spray freeze drying, near critical drying, supercritical drying, and nitrogen gas drying.
  • the crystallization method of the invention may further comprise the step of exchanging the crystallization mother liquor with a different buffer, e.g. a buffer containing polyethylene glycol (PEG) with a molar mass in the range of about 300 to 8000 Daltons or mixtures of PEGs, by centrifugation, diafiltration, ultrafiltration or other commonly used buffer exchange techniques.
  • a buffer containing polyethylene glycol (PEG) with a molar mass in the range of about 300 to 8000 Daltons or mixtures of PEGs
  • the present invention also relates to a crystal of an anti-hTNFalpha antibody, obtainable by a crystallization method as defined above and in general to crystals of an anti- hTNFalpha antibody
  • the crystals of the invention are typically characterized by a needle-like morphology with a maximum length I of about 2 - 500 ⁇ m or about 100 - 300 ⁇ m and an l/d ratio of about 3 to 30, but may also have other geometrical appearances
  • Said crystal may be obtained from a polyclonal antibody or, preferably, a monoclonal antibody.
  • said antibody is selected from the group consisting of: non-chimeric or chimeric antibodies, humanized antibodies, non-glycosylated antibodies, human antibodies and mouse antibodies.
  • the antibody to be crystallized is a non- chimeric, human antibody optionally further processed for improving the antigen- binding.
  • said crystals are obtained from an IgG antibody such as, for example, an IgGI , lgG2, lgG3 or lgG4 antibody.
  • said antibody is a whole anti-human TNFalpha antibody of the group IgGI .
  • the crystals are prepared from an isolated human antibody, that dissociates from hTNFalpha with a Kd of 1 x10 "8 M or less, more preferably 1x 10 ⁇ 9 M or less, and even more preferably 5 x 10 ⁇ 10 M or less, and a K a rate constant of 1 x 10 '3 s '1 or less, both determined by surface plasmon resonance, and neutralizes hTNFalpha cytotoxicity in a standard in vitro L929 assay with an IC 50 of 1 x10 '7 M or less.
  • said crystals may be prepared from an isolated human antibody with the following characteristics: a) dissociates from human TNFalpha with a k off rate constant of 1 x 10 '3 s '1 or less, as determined by surface plasmon resonance; b) has a light chain CDR3 domain comprising the amino acid sequence of SEQ ID NO: 3, or modified from SEQ ID NO: 3 by a single alanine substitution at position 1 , 4, 5, 7 or 8, or by one to five conservative amino acid substitutions at positions 1 , 3, 4, 6, 7, 8 and/or 9; c) has a heavy chain CDR3 domain comprising the amino acid sequence of SEQ ID NO: 4, or modified from SEQ ID NO: 4 by a single alanine substitution at position 2, 3, 4, 5, 6, 8, 9, 10 or 11 , or by one to five conservative amino acid substitutions at positions 2, 3, 4, 5, 6, 8, 9, 10, 11 and/or 12.
  • the antibody, or antigen-binding portion thereof dissociates from human TNFalpha with a k o ff of 5 x 10 ⁇ 4 s ⁇ 1 or less. Even more preferably, the antibody, or antigen-binding portion thereof, dissociates from human TNFalpha with a k o ff of 1 x 10- 4 s "1 or less.
  • said crystals are prepared from an isolated human antibody with a light chain variable region (LCVR) comprising the amino acid sequence of SEQ ID NO: 1 and a heavy chain variable region (HCVR) comprising the amino acid sequence of SEQ ID NO: 2.
  • LCVR light chain variable region
  • HCVR heavy chain variable region
  • crystals prepared from the antibody D2E7 as disclosed in WO-A- 97/29131 or a functional equivalent thereof.
  • Said antibody is recombinantly produced in Chinese hamster ovary cells and comprises a heavy chain sequence according to SEQ ID NO:6 and a light chain sequence according to SEQ ID NO: 5.
  • the invention relates to a solid, liquid or semi-solid pharmaceutical composition
  • a solid, liquid or semi-solid pharmaceutical composition comprising: (a) crystals of an anti-hTNFalpha antibody as defined in any one of claims 15 to 26, and (b) at least one pharmaceutically acceptable excipi- ent stably maintaining the antibody crystals.
  • compositions comprising: (a) crystals of an anti-hTNFalpha antibody as defined herein, and (b) at least one pharmaceutically acceptable excipient encapsulating or embedding said antibody crystals.
  • the composition may further comprise (c) at least one pharma- ceutically acceptable excipient stably maintaining the antibody crystals.
  • encapsulation and embedding may be implemented in conjunction.
  • compositions may have an antibody crystal concentration higher than about 1 mg/ml, in particular about 200 mg/ml or more, for example about 200 to about 600 mg/ml, or about 300 to about 500 mg/ml.
  • Said excipients may comprise at least one polymeric, optionally biodegradable carrier or at least one oil or lipid carrier.
  • Said polymeric carrier may be a polymer selected from one or more of the group consisting of: poly (acrylic acid), poly (cyanoacrylates), poly (amino acids), poly (anhydrides), poly (depsipeptide), poly (esters), poly (lactic acid), poly (lactic-co-glycolic acid) or PLGA 1 poly ( ⁇ -hydroxybutryate), poly (caprolactone), poly (dioxanone); poly (ethyl- ene glycol), poly (hydroxypropyl) methacrylamide, poly (organo) phosphazene, poly (ortho esters), poly (vinyl alcohol), poly (vinylpyrrolidone), maleic anhydride alkyl vinyl ether copolymers, pluronic polyols, albumin, alginate, cellulose and cellulose derivatives, collagen, fibrin, gelatin, hyaluronic acid, oligosaccharides, glycaminoglycans, sulfated polys
  • Said oil (or oily liquid) may be an oil (or oily liquid) selected from one or more of the group consisting of: oleaginous almond oil, corn oil, cottonseed oil, ethyl oleate, isopro- pyl myristate, isopropyl palmitate, mineral oil, light mineral oil, octyldodecanol, olive oil, peanut oil, persic oil, sesame oil, soybean oil, squalane, liquid triglycerides, liquid waxes, higher alcohols.
  • oil or oily liquid
  • Said lipid carrier may be a lipid selected from one or more of the group consisting of: fatty acids and salts of fatty acids, fatty alcohols, fatty amines, mono-, di-, and triglycerides of fatty acids, phospholipids, glycolipids, sterols and waxes and related similar substances. Waxes are further classified in natural and synthetic products. Natural materials include waxes obtained from vegetable, animal or minerals sources such as beeswax, carnauba or montanwax. Chlorinated naphthalenes and ethylenic polymers are examples for synthetic wax products.
  • said composition is an injectable composition comprising anti-hTNFalpha antibody crystals as defined above and having an antibody crystal concentration in the range of about 10 to about 400 or about 50 to about 300 mg/ml.
  • the invention relates to a crystal slurry comprising anti-hTNFalpha antibody crystals as defined above having an antibody crystal concentration higher than about 100 mg/ml, for example about 150 to about 600 mg/ml, or about 200 to about 400 mg/ml.
  • the present invention also relates to a method for treating a mammal comprising the step of administering to the mammal an effective amount of whole anti-hTNFalpha antibody crystals as defined above or an effective amount of the composition as defined above.
  • said composition is administered by parenteral route, oral route, or by injection.
  • the present invention relates to a method of treating a hTNFalpha-related disorder in a subject that comprises administering a therapeutically effective amount of antibody crystals as defined above.
  • said hTNFalpha-related disorder is selected from: an autoimmune disease, in particular rheumatoid arthritis, rheumatoid spondylitis, osteoarthritis and gouty arthritis, an allergy, multiple sclerosis, autoimmune diabetes, autoimmune uveitis and nephrotic syndrome; an infectious disease, transplant rejection or graft-versus-host disease, malignancy, pulmonary disorder, intestinal disorder, car- diac disorder, inflammatory bone disorders, bone resorption disease, alcoholic hepatitis, viral hepatitis, fulminant hepatitis, coagulation disturbances, burns, reperfusion injury, keloid formation, scar tissue formation, pyrexia, periodontal disease, obesity and radiation toxicity; a spondyloarthropathy, a pulmonary disorder, a coronary disorder, a metabolic disorder, anemia, pain, a hepatic disorder, a skin disorder, a nail disorder, or vasculitis, Beh
  • post-streptococcal glomerulonephritis or IgA nephropathy loosening of prostheses, microscopic polyangiitis, mixed connective tissue disorder, multiple myeloma, cancer and cachexia, multiple organ disorder, myelo dysplastic syndrome, orchitism osteoly- sis, pancreatitis, including acute, chronic, and pancreatic abscess, periodontal disease polymyositis, progressive renal failure, pseudogout, pyoderma gangrenosum, relapsing polychondritis, rheumatic heart disease, sarcoidosis, sclerosing cholangitis, stroke, thoracoabdominal aortic aneurysm repair(TAAA), TNF receptor associated periodic syndrome (TRAPS), symptoms related to Yellow Fever vaccination, inflammatory dis- eases associated with the ear, chronic ear inflammation, or pediatric ear inflammation, uveitis, sciatica, prostatitis, endo
  • the present invention relates to the use of whole anti-hTNFalpha antibody crystals as defined above for preparing a pharmaceutical composition for treating a hTNFalpha-related disease as defined above.
  • the present invention provides anti-hTNFalpha antibody crystals as defined above for use in medicine.
  • Fig. 1 D2E7 crystals from Example 37 after 6 days.
  • Fig. 2 D2E7 crystals manufactured in 1 mL batch volume, ambient temperature.
  • Fig. 3 D2E7 crystals manufactured in 50 mL batch volume, ambient temperature.
  • Fig. 4 D2E7 crystals manufactured in 10 L batch volume, ambient temperature.
  • Fig. 5 D2E7 crystals manufactured according to the invention and birefringence thereof.
  • Fig. 6 D2E7 crystal suspensions at different concentrations injected via different gauge needles.
  • Fig. 7 FT-IR analysis of D2E7 crystal suspension.
  • a "batch method of crystallization” comprises the step of adding the crystallization solution comprising the crystallization agent, preferably in dissolved form, to the solution of the antibody to be crystallized.
  • a "micro scale crystallization method” which may for example be based upon vapor diffusion, comprises the steps of admixing a small volume of antibody solution in the microliter range with a reservoir buffer containing a crystallization agent; placing a droplet of said mixture in a sealed container adjacent to an aliquot of said reservoir buffer; allowing exchange of solvent between the droplet and the reservoir by vapor diffusion, during which the solvent content in said droplet changes and crystallization may be observed if suitable crystallization conditions are reached.
  • a “crystallization agent” in the present case a phosphate salt, favors crystal formation of the antibody to be crystallized.
  • a “crystallization solution” contains said crystallization agent in dissolved form.
  • said solution is an aqueous system, i.e. the liquid constituents thereof predomi- nantly, consist of water.
  • 80 to 100 wt.-% or 95 to 100 wt.-% or 98 to 100 wt.-% may be water.
  • Antibody crystals are one form of the solid state of matter of said protein, which is distinct from a second solid form, i.e. the amorphous state, which exists essentially as an unorganized, heterogeneous solid. Crystals have a regular three-dimensional structure, typically referred to as a lattice. An antibody crystal comprises a regular three- dimensional array of antibody molecules. See Giege, R. and Ducruix, A. Barrett, Crystallization of Nucleic Acids and Proteins, a Practical Approach, 2nd ed., pp. 1-16, Oxford University Press, New York (1999).
  • a “whole” or “intact” anti-hTNFalpha antibody as crystallized according to this invention is a functional antibody that is able to recognize and bind to its antigen human TNFaI- pha in vitro and/or in vivo.
  • the antibody may initiate subsequent immune system reactions of a patient associated with antibody-binding to its antigen, in particular Direct Cytotoxicity, Complement-Dependent Cytotoxicity (CDC), and Antibody-Dependent Cytotoxicity (ADCC).
  • the antibody molecule has a structure composed of two identical heavy chains (MW each about 50 kDa) covalently bound to each other, and two identical light chains (MW each about 25 kDa), each covalently bound to one of the heavy chains.
  • Each heavy chain is com- prised of a heavy chain variable region (abbreviated herein as HCVR or VH) and a heavy chain constant region.
  • the heavy chain constant region is comprised of three domains, CH1 , CH2 and CH3.
  • Each light chain is comprised of a light chain variable region (abbreviated herein as LCVR or VL) and a light chain constant region.
  • the light chain constant region is comprised of one domain, CL.
  • the VH and VL regions can be further subdivided into regions of hypervariability, termed complementarity determining regions (CDR), interspersed with regions that are more conserved, termed framework regions (FR).
  • CDR complementarity determining regions
  • Each VH and VL is composed of three CDRs and four FRs, arranged from amino-terminus to carboxy-terminus in the following order: FR1 , CDR1 , FR2, CDR2, FR3, CDR3, FR4.
  • the complete antibody molecule has two antigen binding sites, i.e. is "bivalent”.
  • the two antigen binding sites are specific for one hTNFalpha antigen, i.e. the antibody is "mono-specific".
  • Monoclonal antibodies are antibodies that are derived from a single clone of B lymphocytes (B cells), and recognize the same antigenic determinant. Whole monoclonal antibodies are those that have the above-mentioned classic molecular structure that includes two complete heavy chains and two complete light chains. Monoclonal antibodies are routinely produced by fusing the antibody-producing B cell with an immortal myeloma cell to generate B cell hybridomas, which continually produce monoclonal antibodies in cell culture.
  • the monoclonal antibodies to be crystallized according to the invention include "chimeric" anti-hTNFalpha antibodies in which a portion of the heavy and/or light chain is identical with or homologous to corresponding sequences in antibodies derived from a particular species or belonging to a particular antibody class or subclass, while the remainder of the chain(s) is identical with or homologous to corresponding sequences in antibodies derived from another species or belonging to another antibody class or subclass.
  • a mouse/human chimera containing variable antigen-binding portions of a murine antibody and constant portions derived from a human antibody.
  • Humanized forms of non-human (e.g. murine) anti-hTNFalpha antibodies are also encompassed. These are chimeric antibodies that contain minimal sequence derived from a non-human immunoglobulin.
  • humanized antibodies are hu- man immunoglobulins in which residues from a complementarity determining region (CDR) or hypervariable loop (HVL) of the human immunoglobulin are replaced by residues from a CDR or HVL of a non-human species, such as mouse, rat, rabbit or non- human primate, having the desired functionality.
  • Framework region (FR) residues of the human immunoglobulin may replaced by corresponding non-human residues to improve antigen binding affinity.
  • humanized antibodies may comprise residues that are found neither in the corresponding human or non-human antibody portions. These modifications may be necessary to further improve antibody efficacy.
  • human antibody or “fully human antibody” is one, which has an amino acid se- quence which corresponds to that of an antibody produced by a human or which is recombinantly produced.
  • the term "human antibody”, as used herein, is intended to include antibodies having variable and constant regions derived from human germline immunoglobulin sequences.
  • the human antibodies of the invention may include amino acid residues not encoded by human germline immunoglobulin sequences (e.g. muta- tions introduced by random or site-specific mutagenesis in vitro or by somatic mutation in vivo), for example in the CDRs and in particular CDR3.
  • human antibody is not intended to include antibodies in which CDR sequences derived from the germline of another mammalian species, such as a mouse, have been grafted onto human framework sequences.
  • recombinant human antibody is intended to include all human antibodies that are prepared, expressed, created or isolated by recombinant means, such as antibodies expressed using a recombinant expression vector trans- fected into a host cell, antibodies isolated from a recombinant, combinatorial human antibody library, antibodies isolated from an animal (e.g. a mouse) that is transgenic for human immunoglobulin genes (see e.g. Taylor, L.D., et al. (1992) Nucl.
  • Such recombinant human antibodies have variable and constant regions derived from human germline immunoglobulin sequences. In certain embodiments, however, such recombinant human antibodies are subjected to in vitro mutagenesis (or, when an animal transgenic for human Ig sequences is used, in vivo somatic mutagenesis) and thus the amino acid sequences of the VH and VL regions of the recombinant antibodies are sequences that, while derived from and related to human germline VH and VL sequences, may not naturally exist within the human antibody germline repertoire in vivo.
  • a “neutralizing antibody”, as used herein is intended to refer to an antibody whose binding to hTNFalpha results in in- hibition of the biological activity of hTNFalpha.
  • This inhibition of the biological activity of hTNFalpha can be assessed by measuring one or more indicators of hTNFalpha biological activity, such as hTNFalpha-induced cytotoxicity (either in vitro or in vivo), hTNFalpha-induced cellular activation and hTNFalpha binding to hTNFalpha receptors.
  • indicators of hTNFalpha biological activity can be assessed by one or more of several standard in vitro or in vivo assays known in the art.
  • the ability of an antibody to neutralize hTNFalpha activity is assessed by inhibition of hTNFalpha- induced cytotoxicity of L929 cells.
  • the ability of an antibody to inhibit hTNFalpha-induced expression of ELAM-1 on HUVEC, as a measure of hTNFalpha-induced cellular activation can be assessed.
  • an "affinity matured" anti-hTNFalpha antibody is one with one or more alterations in one or more hypervariable regions, which result in an improvement in the affinity of the antibody for antigen, compared to a parent antibody.
  • Affinity matured antibodies will have nanomolar or even picomolar affinities values for the target antigen.
  • Affinity ma- tured antibodies are produced by procedures known in the art. Marks et al., Bio/Technology 10:779-783 (1992) describes affinity maturation by VH and VL domain shuffling. Random mutagenesis of CDR and/or framework residues is described by: Barbas et al., Proc. Nat. Acad. Sci.
  • an "isolated antibody”, as used herein, is intended to refer to an antibody that is substantially free of other antibodies having different antigenic specificities (e.g. an isolated antibody that specifically binds hTNFalpha is substantially free of antibodies that spe- cifically_bind antigens other than hTNFalpha).
  • An isolated antibody that specifically binds hTNFalpha may, however, have cross-reactivity to other antigens, such as hTNFalpha molecules from other species.
  • an isolated antibody may be substantially free of other cellular material and/or chemicals.
  • human TNFalpha (abbreviated herein as hTNFalpha, or simply hTNF), as used herein, is intended to refer to a human cytokine that exists as a 17 kDa secreted form and a 26 kDa membrane-associated form, the biologically active form of which is composed of a trimer of noncovalently bound molecules.
  • hTNFalpha The structure of hTNFalpha is described further in, for example, Pennica, D., et al. (1984) Nature 312:724-729; Davis, J.M., et al. (1987) Biochemistry 26:1322-1326; and Jones, E. Y., et al. (1989) Nature 338:225-228.
  • human TNFalpha is intended to include recombinant human TNFalpha (rhTNFalpha), which can be prepared by standard recombinant expression methods or purchased commercially (R & D Systems, Catalog No. 210-TA, Minneapolis, MN).
  • rhTNFalpha recombinant human TNFalpha
  • k o ff is intended to refer to the off rate constant for dissociation of an antibody from the antibody/antigen complex.
  • K ⁇ j is intended to refer to the dissociation constant of a particular antibody-antigen interaction.
  • a “functional equivalent" of a specific "parent" anti-hTNFalpha antibody as crystallized according to the invention is one which shows the same antigen-specificity, differs however with respect to the molecular composition of the "parent” antibody on the amino acid level or glycosylation level. Said differences, however, may be merely such that the crystallization conditions do not deviate from the parameter ranges as disclosed herein.
  • Encapsulation of antibody crystals refers to a formulation where the incorporated crystals are individually coated by at least one layer of a coating material. In a preferred embodiment, such coated crystals may have a sustained dissolution rate.
  • Embedding of antibody crystals refers to a formulation where the crystals, which might be encapsulated or not, are incorporated into a solid, liquid or semi-solid carrier in a disperse manner. Such embedded crystallized antibody molecules may be released or dissolved in a controlled, sustained manner from the carrier.
  • the crystallization method of the invention is in principle applicable to any anti- hTNFalpha antibody.
  • Said antibody may be a polyclonal antibody or, preferably, a monoclonal antibody.
  • Said antibody may be chimeric antibodies, humanized antibodies, human antibodies or non-human, as for example mouse antibodies, each in glyco- sylated or non-glycosylated form.
  • the method is applicable to D2E7 and functional equivalents thereof.
  • said anti-hTNFalpha antibody is an IgG antibody, in particular an anti human TNFalpha antibody of the group IgGL
  • the crystallization method of the invention makes use of technical equipment, chemicals and methodologies well known in the art.
  • the present invention is based on the surprising finding that the selection of specific crystallization conditions, in particular, the selection of specific crystalli- zation agents, optionally further combined with specific pH conditions and/or concentration ranges of the corresponding agents (buffer, antibody, crystallization agent), allows for the first time to prepare reproducibly and in a large scale stable crystals of antibodies, in particular non-chimeric, human antibodies, directed against hTNF alpha, which can be further processed to form an active ingredient of a superior, highly advanta- geous pharmaceutical composition.
  • the starting material for performing the crystallization method normally comprises a concentrated solution of the antibody to be crystallized.
  • the protein concentration may, for example, be in the range of about 5 to 75 mg/ml.
  • Said solution may contain addi- tives stabilizing said dissolved antibody, and it may be advisable to remove said additives in advance. This can be achieved by performing a buffer exchange step.
  • said starting material for performing the crystallization contains the antibody in an aqueous solution, having a pH adjusted in the range of about 3.2 to 8.2, or about 4.0 to 8.0, in particular about 4.5 to 6.5, preferably around 5.0 to 5.5.
  • the pH may be adjusted by means of a suitable buffer applied in a final concentration of about 1 to 50 mM, in particular about 1 to 10 mM.
  • the solution may contain additives, as for example in a proportion of about 0.01 to 15, or 0.1 to 5, or 0.1 to 2 wt.-% based on the total weight of the solution, like salts, sugars, sugar alcohols and surfactants, in order to further stabilize the solution.
  • the excipients should preferably be selected from physiologically acceptable compounds, routinely applied in pharmaceutical preparations.
  • physiologically acceptable compounds such as NaCI;; surfactants, like poly- sorbate 80 (Tween 80), polysorbate 20 (Tween 20); sugars, like sucrose, trehalose; sugar alcohols, like mannitol, sorbitol; and buffer agents, like phosphate-based buffer systems, as sodium and potassium hydrogen phosphate buffers as defined above, acetate buffer, phosphate buffer, citrate buffer, TRIS buffer, maleate buffer or succinate buffer, histidine buffer; amino acids, like histidine, arginine and glycine.
  • salts like NaCI
  • surfactants like poly- sorbate 80 (Tween 80), polysorbate 20 (Tween 20)
  • sugars like sucrose, trehalose
  • sugar alcohols like mannitol, sorbitol
  • buffer agents like phosphate-based buffer systems, as sodium and potassium hydrogen phosphate buffer
  • the buffer exchange may be performed by means of routine methods, for example dialysis or ultrafiltration.
  • the initial protein concentration of the aqueous solution used as starting material should be in the range of about 0.5 to about 200 or about 1 to about 50 mg/ml.
  • an initial volume of said aqueous antibody solution is placed in an appropriate container (as for example a vessel, bottle or tank) made of inert material, as for example glass, polymer or metal.
  • the initial volume of said aqueous solution may correspond to about 30 to 80%, normally about 50% of the final batch size. If necessary the solution after having been filled into said container will be brought to standardized conditions. In particular, the temperature will be adjusted in the range of about 4 0 C and about 37 0 C.
  • the crystallization solution containing the crystallization agent in an appropriate concentration, optionally pre-conditioned in the same way as the antibody solution, is added to the antibody solution.
  • the addition of the crystallization solution is performed continuously or discontinuously optionally under gentle agitation in order to facilitate mixing of the two liquids.
  • the addition is performed under conditions where the protein solution is provided under agitation and the crystallization solution (or agents in its solid from) is / are added in a controlled manner.
  • the formation of the antibody crystals is initiated by applying a phosphate salt, in particular a hydrogen phosphate salt, and preferably an alkali metal salt, or a mixture of at least two different alkali metal salts as defined above as the crystallization agent.
  • the crystallization solution contains the agent in a concentration which is sufficient to afford a final concentration of the phosphate salt in said crystallization mixture in the range of about 1 to 6 M.
  • the crystallization solution additionally contains an acidic buffer, i.e. different from that of the antibody solution, in a concentration suitable to allow the adjustment of the pH of the crystallization mixture in the range of about 3 to 5.
  • an acidic buffer i.e. different from that of the antibody solution
  • the thus obtained mixture may be further incubated for about 1 hour to about 60 days in order to obtain a maximum yield of antibody crystals.
  • the mixture may, for example, be agitated, gently stirred, rolled or moved in a manner known per se.
  • the crystals obtained may be separated by known methods, for example filtration or centrifugation, as for example by centrifugation at about 200 - 20000 rpm, preferably 500 - 2000 rpm, at room temperature or 4°C.
  • the remaining mother liquor may be discarded or further processed. If necessary, the thus isolated crystals may be washed and subsequently dried, or the mother liquor can be exchanged by a different solvent system suitable for storage and /or final use of the antibodies suspended therein.
  • Antibody crystals formed according to the present invention may vary in their shape. Shapes typically may include needles, cone-like, spherical and sea urchin like shapes.
  • the size of the crystals can be on the order of higher nm to mm size (as for example length). In some embodiments, the crystals are at least about 10 ⁇ m in size, and may be visible to the naked eye.
  • the size of the crystals will vary depending on the route of administration, for example, for subcutaneous administration the size of the crystals may be larger than for intravenous administration.
  • the shape of the crystals may be altered by adding specific additional additives to the crystallization mixture, as has been previously described for both protein crystals and crystals of low molecular weight organic and inorganic molecules.
  • Crystals of an antibody can be analyzed microscopically for birefringence. In general, crystals, unless of cubic internal symmetry, will rotate the plane of polarization of polar- ized light. In yet another method, crystals can be isolated, washed, resolubilized and analyzed by SDS-PAGE and, optionally, stained with an anti-Fc receptor antibody. Optionally, the resolubilized antibody can also be tested for binding to its hTNFalpha utilizing standard assays.
  • Crystals as obtained according to the invention may also be crosslinked to one another. Such crosslinking may enhance stability of the crystals.
  • Crystals can be crosslinked using a bifunctional reagent such as glutaraldehyde. Once crosslinked, crystals can be lyophilized and stored for use, for example, in diagnostic or therapeutic applications.
  • Crystals may be dried by means of inert gases, like nitrogen gas, vacuum oven drying, lyophilization, evaporation, tray drying, fluid bed drying, spray drying, vacuum drying or roller drying. Suitable methods are well known. Crystals formed according to the invention can be maintained in the original crystallization solution, or they can be washed and combined with other substances, like inert carriers or ingredients to form compositions or formulations comprising crystals of the invention. Such compositions or formulations can be used, for example, in therapeutic and diagnostic applications.
  • inert gases like nitrogen gas, vacuum oven drying, lyophilization, evaporation, tray drying, fluid bed drying, spray drying, vacuum drying or roller drying. Suitable methods are well known. Crystals formed according to the invention can be maintained in the original crystallization solution, or they can be washed and combined with other substances, like inert carriers or ingredients to form compositions or formulations comprising crystals of the invention. Such compositions or formulations can be used, for example, in therapeutic and diagnostic applications.
  • a preferred embodiment is to combine a suitable carrier or ingredient with crystals of the invention in that way that crystals of the formulation are embedded or encapsulated by an excipient.
  • Suitable carriers may be taken from the non limiting group of: poly (acrylic acid), poly (cyanoacrylates), poly (amino acids), poly (anhydrides), poly (dep- sipeptide), poly (esters), poly (lactic acid), poly (lactic-co-glycolic acid) or PLGA, poly ( ⁇ -hydroxybutryate), poly (caprolactone), poly (dioxanone); poly (ethylene glycol), poly (hydroxypropyl) methacrylamide, poly (organo) phosphazene, poly (ortho esters), poly (vinyl alcohol), poly (vinylpyrrolidone), maleic anhydride alkyl vinyl ether copolymers, pluronic polyols, albumin, alginate, cellulose and cellulose derivatives, collagen, fibrin, gelatin, hyaluronic acid,
  • Waxes are further classified in natural and synthetic products.
  • Natural materials include waxes obtained from vegetable, animal or minerals sources such as beeswax, carnauba or montanwax. Chlorinated naphthalenes and ethylenic polymers are examples for synthetic wax products.
  • compositions/formulations comprising anti- hTNFalpha antibody crystals in combination with at least one carrier/excipient.
  • the formulations may be solid, semisolid or liquid.
  • Formulations of the invention are prepared, in a form suitable for storage and/or for use, by mixing the antibody having the necessary degree of purity with a physiologically acceptable additive, like carrier, excipient and/or stabilizer (see for example Rem- ington's Pharmaceutical Sciences, 16th Edn., Osol, A. Ed. (1980)), in the form of sus- pensions, lyophilized or dried in another way.
  • a physiologically acceptable additive like carrier, excipient and/or stabilizer
  • further active ingredients as for example different antibodies, biomolecules, chemically or enzymatically synthesized low-molecular weight molecules may be incorporated as well.
  • Acceptable additives are non-toxic to recipients at the dosages and concentrations employed.
  • Nonlimiting examples thereof include:
  • Acidifying agents like acetic acid, citric acid, fumaric acid, hydrochloric acid, malic acid, nitric acid, phosphoric acid, diluted phosphoric acid, sulfuric acid, tartaric acid.
  • Aerosol propellants like butane, dichlorodifluoromethane, dichlorotetrafluoroethane, isobutane, propane, trichloromonofluoromethane.
  • Alkalizing agents like ammonia solution, ammonium carbonate, diethanolamine, diisopropanolamine, potassium hydroxide, sodium bicarbonate, sodium borate, sodium carbonate, sodium hydroxide, trolamine;
  • Antifoaming agents like dimethicone, simethicone.
  • Antimicrobial preservatives like benzalkonium chloride, benzalkonium chloride solu- tion, benzelthonium chloride, benzoic acid, benzyl alcohol, butylparaben, cetylpyridin- ium chloride, chlorobutanol, chlorocresol, cresol, dehydroacetic acid, ethylparaben, methylparaben, methylparaben sodium, phenol, phenylethyl alcohol, phenylmercuric acetate, phenylmercuric nitrate, potassium benzoate, potassium sorbate, propylparaben, propylparaben sodium, sodium benzoate, sodium dehydroacetate, sodium propi- onate, sorbic acid, thimerosal, thymol.
  • Antioxidants like ascorbic acid, acorbyl palmitate, butylated hydroxyanisole, butylated hydroxytoluene, hypophosphorous acid, monothioglycerol, propyl gallate, sodium formaldehyde sulfoxylate, sodium metabisulfite, sodium thiosulfate, sulfur dioxide, toco- pherol, tocopherols excipient;
  • Buffering agents like acetic acid, ammonium carbonate, ammonium phosphate, boric acid, citric acid, lactic acid, phosphoric acid, potassium citrate, potassium metaphos- phate, potassium phosphate monobasic, sodium acetate, sodium citrate, sodium lac- tate solution, dibasic sodium phosphate, monobasic sodium phosphate, histidine.
  • Chelating agents like edetate disodium, ethylenediaminetetraacetic acid and salts, edetic acid;
  • - Coating agents like sodium carboxymethylcellulose, cellulose acetate, cellulose acetate phthalate, ethylcellulose, gelatin, pharmaceutical glaze, hydroxypropyl cellulose, hydroxypropyl methylcellulose, hydroxypropyl methylcellulose phthalate, methacrylic acid copolymer, methylcellulose, polyethylene glycol, polyvinyl acetate phthalate, shellac, sucrose, titanium dioxide, camauba wax, microcystalline wax, zein, poly amino acids, other polymers like PLGA etc., and SAIB.
  • EDTA ethylenediaminetetraacetic acid and salts
  • Emulsifying and/or solubilizing agents like acacia, cholesterol, diethanolamine (adjunct), glyceryl monostearate, lanolin alcohols, lecithin, mono-and di-glycerides, monoethanolamine (adjunct), oleic acid (adjunct), oleyl alcohol (stabilizer), poloxamer, polyoxyethylene 50 stearate, polyoxyl 35 caster oil, polyoxyl 40 hydrogenated castor oil, polyoxyl 10 oleyl ether, polyoxyl 20 cetostearyl ether, polyoxyl 40 stearate, polysorbate 20, polysorbate 40, polysorbate 60, polysorbate 80, propylene glycol diacetate, propylene glycol monostearate, sodium lauryl sulfate, sodium stearate, sorbitan monolaurate, soritan monooleate, sorbitan monopalmitate, sorbitan monostearate, stearic acid,
  • Filtering aids like powdered cellulose, purified siliceous earth.
  • Flavors and perfumes like anethole, benzaldehyde, ethyl vanillin, menthol, methyl salicylate, monosodium glutamate, orange flower oil, peppermint, peppermint oil, peppermint spirit, rose oil, stronger rose water, thymol, tolu balsam tincture, vanilla, vanilla tincture, vanillin.
  • Glidant and/or anticaking agents like calcium silicate, magnesium silicate, colloidal silicon dioxide, talc.
  • - Humectants like glycerin, hexylene glycol, propylene glycol, sorbitol;
  • Ointment bases like lanolin, anhydrous lanolin, hydrophilic ointment, white ointment, yellow ointment, polyethylene glycol ointment, petrolatum, hydrophilic petrolatum, white petrolatum, rose water ointment, squalane.
  • Plasticizers like castor oil, lanolin, mineral oil, petrolatum, benzyl benyl formate, chlorobutanol, diethyl pthalate, sorbitol, diacetylated monoglycerides, diethyl phthalate, glycerin, glycerol, mono-and di-acetylated monoglycerides, polyethylene glycol, propylene glycol, triacetin, triethyl citrate, ethanol.
  • Polypeptides like low molecular weight (less than about 10 residues); Proteins, such as serum albumin, gelatin, or immunoglobulins;
  • Sorbents like powdered cellulose, charcoal, purified siliceous earth, Carbon dioxide sorbents, barium hydroxide lime, soda lime.
  • Stiffening agents like hydrogenated castor oil, cetostearyl alcohol, cetyl alcohol, cetyl esters wax, hard fat, paraffin, polyethylene excipient, stearyl alcohol, emulsifying wax, white wax, yellow wax.
  • - Suppository bases like cocoa butter, hard fat, polyethylene glycol
  • Suspending and/or viscosity-increasing agents like acacia, agar, alginic acid, aluminum monostearate, bentonite, purified bentonite, magma bentonite, carbomer 934p, carboxymethylcellulose calcium, carboxymethylcellulose sodium, carboxymethycellu- lose sodium 12, carrageenan, microcrystalline and carboxymethylcellulose sodium cellulose, dextrin, gelatin, guar gum, hydroxyethyl cellulose, hydroxypropyl cellulose, hy- droxypropyl methylcellulose, magnesium aluminum silicate, methylcellulose, pectin, polyethylene oxide, polyvinyl alcohol, povidone, propylene glycol alginate, silicon dioxide, colloidal silicon dioxide, sodium alginate, tragacanth, xanthan gum;
  • Sweetening agents like aspartame, dextrates, dextrose, excipient dextrose, fructose, mannitol, saccharin, calcium saccharin, sodium saccharin, sorbitol, solution sorbitol, sucrose, compressible sugar, confectioner's sugar, syrup;
  • - Tablet binders like acacia, alginic acid, sodium carboxymethylcellulose, microcrystalline cellulose, dextrin, ethylcellulose, gelatin, liquid glucose, guar gum, hydroxypropyl methylcellulose, methycellulose, polyethylene oxide, povidone, pregelatinized starch, syrup.
  • diluents like calcium carbonate, dibasic calcium phosphate, tribasic calcium phosphate, calcium sulfate, microcrystalline cellulose, powdered cellulose, dextrates, dextrin, dextrose excipient, fructose, kaolin, lactose, mannitol, sorbitol, starch, pregelatinized starch, sucrose, compressible sugar, confectioner's sugar;
  • - Tablet and/or capsule lubricants like calcium stearate, glyceryl behenate, magnesium stearate, light mineral oil, polyethylene glycol, sodium stearyl fumarate, stearic acid, purified stearic acid, talc, hydrogenated vegetable oil, zinc stearate;
  • - Tonicity agent like dextrose, glycerin, mannitol, potassium chloride, sodium chloride Vehicle: flavored and/or sweetened aromatic elixir, compound benzaldehyde elixir, iso- alcoholic elixir, peppermint water, sorbitol solution, syrup, tolu balsam syrup.
  • - Vehicles like oleaginous almond oil, corn oil, cottonseed oil, ethyl oleate, isopropyl myristate, isopropyl palmitate, mineral oil, light mineral oil, myristyl alcohol, octyldode- canol, olive oil, peanut oil, persic oil, sesame oil, soybean oil, squalane; solid carrier sugar spheres; sterile bacteriostatic water for injection, bacteriostatic sodium chloride injection, liquid triglycerides, liquid waxes, higher alcohols
  • - Wetting and/or solubilizing agents like benzalkonium chloride, benzethonium chloride, cetylpyridinium chloride, docusate sodium, nonoxynol 9, nonoxynol 10, octoxynol 9, poloxamer, polyoxyl 35 castor oil, polyoxyl 40, hydrogenated castor oil, polyoxyl 50 stearate, polyoxyl 10 oleyl ether, polyoxyl 20, cetostearyl ether, polyoxyl 40 stearate, polysorbate 20, polysorbate 40, polysorbate 60, polysorbate 80, sodium lauryl sulfate, sorbitan monolaureate, sorbitan monooleate, sorbitan monopalmitate, sorbitan monostearate, tyloxapol;
  • the crystals may be combined with a polymeric carrier to provide for stability and/or sustained release.
  • a polymeric carrier include biocompatible and biodegradable polymers.
  • a polymeric carrier may be a single polymer type or it may be composed of a mixture of polymer types. Nonlimiting examples of polymeric carriers have already been stated above.
  • ingredients or excipients examples include:
  • amino acids such as glycine, arginine, aspartic acid, glutamic acid, lysine, asparagine, glutamine, proline, histidine;
  • - monosaccharides such as glucose, fructose, galactose, mannose, arabinose, xylose, ribose
  • - disaccharides such as lactose, trehalose, maltose, sucrose
  • - polysaccharides such as maltodextrins, dextrans, starch, glycogen
  • alditols such as mannitol, xylitol, lactitol, sorbitol;
  • cyclodextrins such as methyl cyclodextrin, hydroxypropyl- (3-cyclodextrin) - inorganic salts, such as sodium chloride, potassium chloride, magnesium chloride, phosphates of sodium and potassium, boric acid ammonium carbonate and ammonium phosphate;
  • - organic salts such as acetates, citrate, ascorbate, lactate;
  • - emulsifying or solubilizing agents like acacia, diethanolamine, glyceryl monostearate, lecithin, monoethanolamine, oleic acid, oleyl alcohol, poloxamer, polysorbates, sodium lauryl sulfate, stearic acid, sorbitan monolaurate, sorbitan monostearate, and other sorbitan derivatives, polyoxyl derivatives, wax, polyoxyethylene derivatives, sorbitan derivatives; and
  • - viscosity increasing reagents like, agar, alginic acid and its salts, guar gum, pectin, polyvinyl alcohol, polyethylene oxide, cellulose and its derivatives propylene carbonate, polyethylene glycol, hexylene glycol and tyloxapol.
  • Formulations described herein also comprise an effective amount of crystalline antibody.
  • the formulations of the invention may include a "therapeutically ef- fective amount” or a “prophylactically effective amount” of antibody crystals of the invention.
  • a “therapeutically effective amount” refers to an amount effective, at dosages and for periods of time necessary, to achieve the desired therapeutic result.
  • a “therapeutically effective amount” of the antibody crystals may vary according to factors such as the disease state, age, sex, and weight of the individual, and the ability of the anti- body to elicit a desired response in the individual.
  • a therapeutically effective amount is also one in which any toxic or detrimental effects of the antibody are outweighed by the therapeutically beneficial effects.
  • prophylactically effective amount refers to an amount effective, at dosages and for periods of time necessary, to achieve the desired prophylactic result. Typically, since a prophylactic dose is used in subjects prior to or at an earlier stage of disease, the prophylactically effective amount will be less than the therapeutically effective amount.
  • Suitable dosages can readily be determined using standard methodology.
  • the antibody is suitably administered to the patient at one time or over a series of treatments. De- pending on the above mentioned factors, about 1 ⁇ g/kg to about 50 mg/kg , as for ex- ample 0.1 -20 mg/kg of antibody is an initial candidate dosage for administration to the patient, whether, for example, by one or more separate administrations, or by continuous infusion.
  • a typical daily or weekly dosage might range from about 1 ⁇ g/kg to about 20 mg/kg or more, depending on the condition, the treatment is repeated until a desired suppression of disease symptoms occurs.
  • formulations comprise a concentration of antibody of at least about 1 g/L or greater when resolubilized. In other embodiments, the antibody concentration is at least about 1 g/L to about 100 g/L when resolubilized.
  • Crystals of an antibody, or formulations comprising such crystals may be administered alone or as part of a pharmaceutical preparation. They may be administered by parenteral, oral or topical routes. For example, they may be administered by oral, pulmonary, nasal, aural, anal, dermal, ocular, intravenous, intramuscular, intraarterial, intraperitoneal, mucosal, sublingual, subcutaneous, transdermal, topical or intracranial routes, or into the buccal cavity.
  • Specific examples of administration techniques comprise pulmonary inhalation, intralesional application, needle injection, dry powder inhalation, skin electroporation, aerosol delivery, and needle-free injection technologies, including needle-free subcutaneous administration.
  • Frozen monoclonal antibody (mAb) D2E7 was obtained from Abbott Laboratories. All experiments were performed from a drug product lot where the original mAb concentration was 50 mg/ml.
  • D2E7 solution was placed into a SLI DE-A-LYZER dialysis cassette (Pierce Biotechnology Inc.).
  • the dialysis cassette was placed into a beaker containing the buffer of choice, and the buffer exchange was performed at 4 0 C overnight with stirring. After adjustment of protein concentration, the solution was sterile filtered through a 0.2 ⁇ m syringe driven filter unit.
  • ThermoSpectronics UV1 device was used to assess protein concentration at a wave- length of 280 nm, applying an extinction coefficient of 1.39 cm 2 mg "1 . For this purpose, aliquots of crystallization slurries were centrifuged at 14,000 rpm, and residual protein concentration was determined in the supernatant.
  • pH measurements were conducted by using a Mettler Toledo MP220 pH meter, lnlab 413 electrodes and lnlab 423 microelectrodes were utilized.
  • Batch crystallization - method A (24 well plate) Batch crystallization was performed by admixing the protein solution with an equal amount of crystallization buffer (500 ⁇ l) in a well. The well was subsequently sealed with adhesive tape to prevent water evaporation.
  • Samples were prepared by adjusting protein concentration to 8 ⁇ g / 20 ⁇ l_. The samples were diluted with an SDS / Tris / Glycerine buffer containing bromphenolblue.
  • Crystals were observed using a Zeiss Axiovert 25 or a Nikon Labophot microscope.
  • the latter was equipped with a polarization filter set and a JVC TK C1380 color video camera.
  • Concentration values given in the following examples are initial values referring to the antibody solution and the reservoir solution before mixing of the two solutions.
  • pH values refer to the pH of an acetate buffer stock be- fore it was combined with other substances, like the crystallization agent.
  • All buffer molarities if not described otherwise, refer to sodium acetate concentrations in a stock solution before pH adjustment, typically performed using acetic acid glacial.
  • Example 1 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water (fully desalted and optionally pre-destilled) in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 was varied from around 6% w/v to around 28% w/v in 2% steps.
  • the pH was around 5.2 throughout. Each condition was assessed in duplicate.
  • Example 2 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffu- sion mode, different protein concentration
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 50 mg/mL. Except for the protein concentration the process conditions were identical with those of Example 1. RESULTS: From the 24 wells assessed, no crystals were observed.
  • Example 3 PEG 400 / sodium acetate grid screen in hanging drop vapor diffu- sion mode
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 400 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 400 was varied from around 30% w/v to around 40% w/v in 2% steps.
  • the pH was around 5.2 throughout.
  • Each condition was assessed in duplicate.
  • Around 1 ⁇ l_ of protein solution was admixed with around 1 ⁇ l_ of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were stored at ambient temperature. Microscopy of the drops was performed multiple times during the following thirty days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 4 PEG 400 / sodium acetate grid screen in hanging drop vapor diffusion mode, different protein concentration
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 50 mg/mL. Except for the protein concentration the process conditions were identical with those of Example 3.
  • Example 5 PEG 10,000 / sodium acetate grid screen in hanging drop vapor diffusion mode
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 400 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 10,000 was varied from around 4% w/v to around 14% w/v in 2% steps.
  • the pH was around 5.2 throughout.
  • Each condition was assessed in duplicate.
  • Around 1 ⁇ l_ of protein solution was admixed with around 1 ⁇ l_ of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were stored at ambient temperature. Microscopy of the drops was performed multiple times during the following thirty days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 6 PEG 10,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different protein concentration
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 45 to 55 mg/mL, preferably 50 mg/mL. Except for the protein concentration the process conditions were identical with those of Example 5.
  • Example 7 PEG 400 / sodium acetate grid screen in hanging drop vapor diffu- sion mode, different set up D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2. The protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 10,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 400 was around 32% w/v and around 34% w/v.
  • the pH was around 4.2, 4.7, 5.2, 5.7, 6.2 or 6.7. Each condition was assessed in duplicate.
  • Example 8 PEG 400 / sodium acetate grid screen in hanging drop vapor diffusion mode, different protein concentration and set up
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 50 mg/mL. Except for the protein concentration the process conditions were identical with those of Example 7.
  • Example 9 PEG 400 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 400 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was used at around 0.025 M, 0.05 M 1 0.075 M 1 0.15 M, 0.2 M or 0.25 M.
  • PEG 400 was varied from around 32% w/v to around 34% w/v.
  • the pH was around 5.7 or 4.2. Each condition was assessed in duplicate.
  • Example 10 PEG 400 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ L of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 400 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was used at around 0.025 M, 0.05 M or 0.1 M.
  • PEG 400 was around 28% w/v or around 30% w/v.
  • the pH was around 5.2, 5.7, 6.2 or 6.7. Each condition was assessed in duplicate.
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 was varied from around 4% w/v to around 8% w/v in 2% steps.
  • PEG 400 was added to the PEG 4,000 / acetate solutions at concentrations of around 24% w/v, 26% w/v, 28% w/v or 30% w/v.
  • the pH was around 5.2 throughout. Each condition was assessed in duplicate.
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.2.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ L of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 was varied from around 4% w/v to around 8% w/v in 2% steps.
  • PEG 400 was added to the PEG 4,000 / acetate solutions at concentrations of around 30% w/v, 32% w/v, 34% w/v or 36% w/v.
  • the pH was around 4.2 throughout.
  • Each condition was assessed in duplicate.
  • Around 1 ⁇ L of protein solution was admixed with around 1 ⁇ L of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were stored at ambient temperature. Microscopy of the drops was performed multiple times during the following thirty days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 13 PEG 4,000 / sodium acetate grid screen in hanging drop vapor dif- fusion mode, different set up
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 6.5, 6.0, 5.5, 5.0, 4.5 or 4.0.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ L of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 was varied from around 4% w/v to around 26% w/v in 2% steps.
  • the pH of the acetate buffer used was the same as the corresponding protein buffer. Each condition was assessed in duplicate.
  • Example 14 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • Example 15 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • Example 13 The experimental conditions were identical to Example 13, except for the acetate buffer molarity which was kept constant at 0.1 M (molarity of precipitation buffer).
  • Example 16 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • Example 13 The experimental conditions were identical to Example 13, except for the acetate buffer molarity which was kept constant at around 0.4 M (molarity of precipitation buffer).
  • Example 17 - PEG 4,000 / sodium acetate bulk experiments D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.5. The protein concentration was adjusted to 10 mg/mL.
  • Example 18 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different temperature
  • Example 13 The experimental conditions were identical to Example 13. However, the tubes were set up and stored at 4 0 C.
  • Example 19 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different protein concentration
  • Example 20 Ammonium sulfate / sodium acetate grid screen in hanging drop vapor diffusion mode D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.5. The protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, ammonium sulfate stock solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and the ammonium sulfate concentration was varied from 0.5 M to 2.5 M in steps of 0.25 M.
  • the pH of the acetate buffer was around 5.5 throughout. Each condition was assessed in duplicate.
  • Around 1 ⁇ L of protein solution was admixed with around 1 ⁇ L of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were set up and stored at ambient temperature. Microscopy of the drops was performed multiple times during the follow- ing two weeks. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 21 Sodium chloride / sodium acetate grid screen in hanging drop vapor diffusion mode
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.5.
  • the protein concentration was adjusted to 10 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ L of a particular reservoir solution was prepared by admixing acetate buffer, sodium chloride stock solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and the sodium chloride concentration was varied from 1.5 M to 2.5 M 1 varied in steps of 0.5 M.
  • the pH of the acetate buffer was around 5.5 throughout.
  • Each condition was assessed in duplicate.
  • Around 1 ⁇ L of protein solution was admixed with around 1 ⁇ L of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were set up and stored at ambient temperature. Microscopy of the drops was performed multiple times during the following two weeks. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 22 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, influence of detergents
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.5.
  • the protein concentration was adjusted to 5 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 was varied from around 10% w/v to around 20% w/v in 2% steps.
  • the pH of the acetate buffer was around 5.5 throughout.
  • polysorbate 20, polysorbate 80 and Pluronic F 68 were added to any resulting buffer as described above at concentrations of 0%, 0.02% and 0.1 %, respectively.
  • D2E7 was buffered into a buffer containing around 0.1 M sodium acetate at a pH of around 5.5.
  • the protein concentration was adjusted to 10 mg/mL
  • a greased VDX plate and square OptiClear plastic cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, zinc acetate stock solution and MiIIi Q water in each well.
  • the acetate buffer molar- ity was kept constant at around 0.1 M, and the zinc acetate concentration was varied from 0.1 M to 0.9 M in steps of around 0.2 M.
  • the pH of the acetate buffer was around 5.5 throughout.
  • Each condition was assessed in duplicate.
  • Around 1 ⁇ l_ of protein solution was admixed with around 1 ⁇ l_ of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were set up and stored at ambient temperature. Microscopy of the drops was performed multiple times during the following two weeks. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated
  • Example 24 Broad screening of conditions in vapor diffusion mode
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4.
  • the protein concentration was adjusted to 5 mg/mL, 10 mg/mL, or 20 mg/mL.
  • 96 well Greiner plates were set up at ambient temperature, using several commercially available crystallization screens.
  • the protein solution and the crystallization agent were admixed in a ratio of around 1 :1 , preferably 1 :1.
  • the plates were sealed with Clearseal film. Each plate was set up in quadruplicate and then stored at ambient temperature, 4 °C, 27 0 C and 37 0 C, respectively. Microscopy of the drops was performed after five days and twelve days, respectively. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • the crystals showed needle cluster-like morphologies.
  • Example 25 PEG 4,000 / sodium acetate grid screen in hanging drop vapor diffusion mode, different set up
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4.
  • the protein concentration was adjusted to 5 mg/mL, 10 mg/mL, or 20 mg/mL.
  • a greased VDX plate and circle siliconized glass cover slides were used.
  • 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well.
  • the acetate buffer molarity was kept constant at around 0.1 M, and PEG 4,000 concentration was varied from 4% to 26% in 2% steps.
  • the pH was around 5.5 throughout.
  • Each condition was set up with the three protein concentrations as described above.
  • Around 1 ⁇ L of protein solution was admixed with around 1 ⁇ L of a particular reservoir solution on a circle sili- conized glass cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were stored at ambient temperature. Microscopy of the drops was performed after six days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 5 mg/mL. A greased VDX plate and circle siliconized glass cover slides were used. 500 ⁇ l_ of a particular reservoir solution was prepared by admixing acetate buffer, 50% w/v PEG 4,000 solution and MiIIi Q water in each well. In this example, the acetate buffer molarity was kept constant at around 0.1 M, and the PEG 4,000 concentration around 12% w/v or 14% w/v. The pH was around 5.5 throughout.
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 5 mg/mL or 10 mg/mL.
  • Greased VDX plates and circle siliconized glass cover slides were used. 500 ⁇ l_ of each of the 48 buffer formulations was pipetted into a well and admixed wit 250 ⁇ L of MiIIi Q water, respectively. Around 1 ⁇ L of protein sample was pipetted onto a cover slide and subsequently admixed with around 1 ⁇ L of the reservoir solution of a particular well. The well was sealed with the inverted cover slide, generating a hanging drop experiment. The plates were stored at ambient temperature. Microscopy of the drops was performed multiple times during the following seven days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 5 mg/mL.
  • Example 27 The experimental conditions were identical with those of Example 27 with the exception that 500 ⁇ L of each of the 48 buffer formulations was pipetted into a well and admixed with 500 ⁇ L of MiIIi Q water, respectively.
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 5 mg/mL.
  • Greased VDX plates and circle siliconized glass cover slides were used. 1 mL of 24% w/v PEG 3,350 dehydrant solution was pipetted into 108 wells, respectively. Around 2 ⁇ L of protein sample were pipetted onto a cover slide and subsequently admixed with around 1 ⁇ L of one of the 18 particular buffer reagents. Thereafter, around 2.5 ⁇ L of PEG 3,350 precipitant of one of six different concentrations was added to the drop. The wells were sealed with the inverted cover slides, generating 108 different hanging drop experiments.
  • the plates were stored at ambient temperature. Microscopy of the drops was per- formed multiple times during the following seven days. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4.
  • the protein concentration was adjusted to 5 mg/mL, 10 mg/mL, or 20 mg/mL.
  • a greased VDX plate and circle siliconized glass cover slides were used. 500 ⁇ L of a particular reservoir solution was prepared by admixing ammonium sulfate stock solu- tion, Bis-Tris propane stock solution and MiIIi Q water in each well. In this example, ammonium sulfate molarity was around 0.5 M, 1 M, 1.5 M or 2 M. The Bis-Tris Propane molarity was 0.1 M throughout, and the Bis-Tris Propane buffer pH was around 5.5, 6.0, 6.5, 7.0, 7.5 or 8.0. The resulting 24 conditions were assessed with all of the three protein concentrations as described above, and with storage at ambient temperature or storage at around 27 0 C, respectively.
  • Example 31 Sodium potassium dihydrogen phosphate / sodium acetate grid screen in hanging drop vapor diffusion mode
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4.
  • the protein concentration was adjusted to 5 mg/mL, 10 mg/mL, or 20 mg/mL.
  • a greased VDX plate and square OptiClear plastic cover slides were used. 500 ⁇ L of a particular reservoir solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and Q water in each well.
  • acetate buffer molarity was kept constant at around 0.1 M
  • the acetate buffer pH was around 4.1 , 4.6, 5.1 or 5.6.
  • the following combinations of sodium dihydrogen phosphate and potassium dihydro- gen phosphate were applied: around 0.3 M sodium dihydrogen phosphate and around 0.3 M potassium dihydrogen phosphate; around 0.6 M sodium dihydrogen phosphate and around 0.6 M potassium dihydrogen phosphate; - around 0.9 M sodium dihydrogen phosphate and around 0.9 M potassium dihydrogen phosphate; around 1.8 M sodium dihydrogen phosphate, around 2.1 M sodium dihydrogen phosphate, around 2.4 M sodium dihydrogen phosphate.
  • Each condition was set up with the three protein concentrations as described above.
  • Around 1 ⁇ l_ of protein solution was admixed with around 1 ⁇ l_ of a particular reservoir solution on a square OptiClear plastic cover slide, and the well was sealed with the inverted slide, generating a hanging drop experiment.
  • the plates were stored at ambi- ent temperature. Microscopy of the drops was performed multiple times during the following month. The conditions were classified into clear drops, drops containing random precipitation, drops containing crystals and drops containing mixtures of precipitated species and crystals.
  • Example 32 Sodium potassium dihydrogen phosphate / sodium acetate grid screen in hanging drop vapor diffusion mode, different temperature
  • Example 31 The experimental conditions were identical with those of Example 31 , except that the storage temperature was increased to 30 0 C.
  • Concentration values given in the following examples are initial values referring to the antibody solution and the crystallization solution before mixing of the two solutions.
  • All buffer molarities refer to sodium acetate concentrations in a stock solution before pH adjustment, typically performed using acetic acid glacial.
  • Example 33 Sodium potassium dihydrogen phosphate / sodium acetate batch crystallization at 800 ⁇ l_ batch volume
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4.
  • the protein concentration was adjusted to 5 mg/mL, 10 mg/mL, or 20 mg/mL.
  • Batch crystallization was performed by admixing around 400 ⁇ L of each protein solution with an equal amount of crystallization solution in a 1.5 mL Eppendorff reaction tube.
  • 400 ⁇ L of a particular crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1.
  • the following combination of sodium dihydrogen phosphate and potassium dihydrogen phosphate was used: around 0.9 M so- dium dihydrogen phosphate and around 0.9 M potassium dihydrogen phosphate.
  • the reaction tubes were stored at ambient temperature. Microscopy of 1 ⁇ l_ aliquots was performed after 11 days.
  • Example 34 Sodium dihydrogen phosphate / sodium acetate batch crystallization at 600 ⁇ L batch volume
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 10 mg/mL.
  • Batch crystallization was performed by admixing around 300 ⁇ L of the protein solution with an equal amount of crystallization solution in a 1.5 mL Eppendorff reaction tube.
  • 300 ⁇ L of a particular crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution and MiIIi Q water.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1.
  • Sodium dihydrogen phosphate molarity was around 1.5 M, 1.8 M, 2.1 M and 2.4 M, respectively.
  • the reaction tubes were stored at ambient temperature. Microscopy of 1 ⁇ L ali- quots was performed after 11 days.
  • Example 35 Sodium potassium dihydrogen phosphate / sodium acetate grid screen batch crystallization at 1 mL batch volume
  • D2E7 was used without exchanging the buffer.
  • the initial composition was D2E7
  • D2E7 was brought to a concentration of around 10 mg/mL by dilution with MiIIi Q water.
  • Batch crystallization was performed by admixing around 500 ⁇ L of the protein solution with an equal amount of crystallization solution in well of a 24 well plate.
  • 500 ⁇ L of a particular crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water in a well.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1 , 4.6, 5.1 or 5.6.
  • the following combinations of sodium dihydrogen phosphate and potassium dihydrogen phosphate were used:
  • the wells were subsequently sealed after preparation of the crystallization mixture to prevent water evaporation. Microscopy of the plate was performed after 4 days.
  • Example 36 Sodium potassium dihydrogen phosphate / sodium acetate grid screen batch crystallization at 1 mL batch volume
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 10 mg/mL.
  • Batch crystallization was performed by admixing around 500 ⁇ L of the protein solution with an equal amount of crystallization solution in well of a 24 well plate.
  • 500 ⁇ L of a particular crystallization solution was prepared by admixing acetate buffer, sodium di- hydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water in a well.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1 or 4.6.
  • the following combinations of sodium dihydrogen phosphate and potassium dihydrogen phosphate were applied:
  • the wells were subsequently sealed after preparation of the crystallization mixture to prevent water evaporation. Microscopy of the plate was performed multiple times during the following week. Furthermore, the crystal yield of three batches was determined by OD280. An aliquot of the suspension was centrifuged at 14,000 rpm, and the protein concentration in the supernatant was assessed.
  • Crystal yield was assessed for the batches at acetate buffer pH 4.1 and sodium dihydrogen phosphate molarity of around 4.0 M to around 4.4 M.
  • the crystal yield as de- termined by OD280 from residual protein concentration in the supernatant was above 95% after five days.
  • Precipitated species were obviously present in these batches immediately after combining the protein solution and the crystallization solution (milky suspension, typical light microscopic picture). As no precipitated species were observed after five days, it was concluded that formerly precipitated species rearranged into crystalline species.
  • the protein is highly supersaturated in the crystallization mixture, and protein precipitates immediately. Some protein may still be dissolved, now either only slightly supersaturated or perhaps even below saturation. Crystals form, thereby further lowering the concentration of dissolved protein. Furthermore, the precipitated species clearly redis- solve over time and are incorporated into the growing crystals.
  • Example 37 sodium dihydrogen phosphate / sodium acetate grid screen batch crystallization at 1 mL batch volume, different protein concentration
  • D2E7 was brought to a concentration of around 10 mg/mL by diluting the liquid with MiIIi Q water.
  • Batch crystallization was performed by admixing around 500 ⁇ l_ of the protein solution with an equal amount of crystallization solution in well of a 24 well plate.
  • 500 ⁇ l_ of a particular crystallization solution was prepared by admixing acetate buffer, sodium di- hydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water in a well.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1 or 4.6.
  • Sodium dihydrogen phosphate molarity was varied from around 2.6 M sodium dihydrogen phosphate to around 4.4 M sodium dihydrogen phosphate in 0.2 M steps.
  • the wells were subsequently sealed after prepa- ration of the crystallization mixture to prevent water evaporation. Microscopy of the plate was performed multiple times during the following week. Furthermore, the crystal yield of one particular batch was determined by OD280. An aliquot of the suspension was centrifuged at 14,000 rpm, and the protein concentration in the supernatant was assessed.
  • Crystal yield was assessed for the batch at acetate buffer pH 4.1 and sodium dihydro- gen phosphate molarity of around 4.2 M. The crystal yield as determined by OD280 from residual protein concentration in the supernatant was above 95% after eight days.
  • Precipitated species were obviously present in these batches immediately after combining the protein solution and the crystallization solution (milky suspension, typical light microscopic picture). As no precipitated species were observed after six days, it was concluded that a phase transition occured where formerly precipitated species rearranged into crystalline species.
  • Example 38 sodium dihydrogen phosphate / sodium acetate batch crystallization at 2 ml. batch volume
  • D2E7 was buffered into a 20 mM HEPES / 150 mM sodium chloride buffer at pH 7.4. The protein concentration was adjusted to 10 mg/mL.
  • Batch crystallization was performed by admixing around 1 ml_ of the protein solution with an equal amount of crystallization solution in a 2 ml_ Eppendorff reaction tube.
  • 1 ml_ of a particular crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution and MiIIi Q water.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1
  • Sodium dihydrogen phosphate molarity was around 4.0 M, 4.2 M or 4.4 M.
  • the reaction tubes were stored at ambient temperature. Microscopy of 1 ⁇ l_ aliquots was performed multi- pie times during the following week.
  • Precipitated species were obviously present in these batches immediately after com- bining the protein solution and the crystallization solution (milky suspension, typical light microscopic picture). Formerly precipitated species rearranged into crystalline species as described in Example 36.
  • Example 39 sodium dihydrogen phosphate / sodium acetate grid screen batch crystallization at 1 ml_ batch volume, different protein concentration
  • Batch crystallization was performed by admixing around 500 ⁇ l_ of the protein solution with an equal amount of crystallization solution in well of a 24 well plate.
  • 500 ⁇ l_ of a particular crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water in a well.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1.
  • Sodium dihydrogen phosphate molarity was varied from around 0.2 M to around 4.4 M in 0.2 M steps.
  • the wells were subsequently sealed after preparation of the crystallization mixture to prevent water evaporation.
  • Microscopy of the plate was performed multiple times during the following week. Further- more, the crystal yield of the batch was determined by OD280. An aliquot of the suspension was centrifuged at 14,000 rpm, and the protein concentration in the supernatant was assessed.
  • sodium dihydrogen phosphate molarity of around 3.4 M and around 3.6 M sodium dihydrogen phosphate molarity of around 3.4 M and around 3.6 M.
  • Example 40 sodium dihydrogen phosphate / sodium acetate batch crystallization at 20 mL batch volume, agitation
  • D2E7 was brought to a concentration of around 10 mg/mL by dilution with MiIIi Q water.
  • Batch crystallization was performed by admixing around 10 mL of protein solution with an equal amount of crystallization solution in a 50 mL Falcon tube.
  • 10 mL of the crystal- lization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution and MiIIi Q water in the tube.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1
  • Sodium dihydrogen phosphate molarity was 4.2 M.
  • the tube was stored at ambient temperature, agitating the batch on a laboratory shaker. Microscopy of a 1 ⁇ L aliquot of the solution was performed multiple times during the following month.
  • Example 41a Sodium dihydrogen phosphate / sodium acetate batch crystallization at 100 mL batch volume, no agitation
  • D2E7 was brought to a concentration of around 10 mg/mL by dilution with MiIIi Q water.
  • Batch crystallization was performed by admixing around 50 mL of protein solution with an equal amount of crystallization solution in a clean 1 L polypropylene bottle.
  • 50 mL of the crystallization solution was prepared by admixing acetate buffer, sodium dihydrogen phosphate stock solution and MiIIi Q water in the tube.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1
  • Sodium dihydrogen phosphate molarity was 4.2 M.
  • the container was stored at ambient temperature. Microscopy of a 1 ⁇ L aliquot of the solution was performed multiple times during the following month.
  • D2E7 Large-scale crystallization of D2E7 was also performed by combining 1 L of 50 mg/mL D2E7 in Adalimumab commercial buffer formulation pH 5.2 (see Example 35) and 4 L water for injection (WFI) in a 10 L polypropylene vessel (Nalgene®). The solution was homogenized by gentle shaking. This 5 L D2E7 solution (10 mg/mL) was then mixed with 5 L of precipitating agent solution (5 M sodium dihydrogen phosphate, 4,400 mL, 1 M sodium acetate buffer, pH 4.1 , 500 mL, WFI (Ampuwa), 100 mL) The precipitating agent solution was added in 500 mL portions. After addition of each portion the solution was homogenized by gently rotating/inverting the bottle. After addition of around 2,500 to -3,000 mL of the precipitating agent solution, a white precipitate appeared. The re- maining precipitating agent was added all at once. Then the crystal preparation was homogenized (gently rotating/inverting
  • D2E7 was successfully crystallized at 100 mL batch volume with ultimately high yield (> 95%) and reproducibility, indicating that this crystallization system is applicable for industrial processing.
  • SDS-PAGE analysis the protein character of the crystals was proven.
  • SE-HPLC analysis of redissolved crystals showed only a slight increase in ag- gregated species. Washing of the crystals was possible by using an acetate buffer containing sodium dihydrogen phosphate around 4.2M sodium dihydrogen phosphate in around 0.1 M sodium acetate at a pH around 4.1. No measurable solubility of D2E7 crystals in such a washing buffer occurs, as analyzed by OD280, recovering more than 90% of the crystals.
  • the crystal slurry was transferred into a centrifugation tube and centrif uged at 500 to 1000 x g for twenty minutes.
  • the centrifugation was performed at 4 0 C, but might also be performed at other feasible temperatures, e.g. room temperature.
  • the supernatant was discarded, and the crystal pellet was resuspended in a buffer containing around 4.2 M sodium dihydrogen phosphate in around 0.1 M sodium acetate at a pH around 4.1. No measurable solubility of D2E7 crystals in the washing buffer occured, as analyzed by OD280.
  • the centrifugation / resuspension steps were subsequently repeated for one to three times, and after this washing procedure, the pellet was re- suspended and stored in a buffer containing around 4.2 M sodium dihydrogen phosphate in around 0.1 M sodium acetate at a pH around 4.1.
  • the crystals were washed with a washing buffer as described in example 42. After assuring by OD280 that no more dissolved protein was present in the supernatant after centrifugation, the supernatant was dis- carded, and the crystals were subsequently dissolved in distilled water. OD280 measurement of this solution revealed that the crystals essentially consisted of protein, as the absorbance of the sample was now significantly higher as in the residual washing buffer. SDS-PAGE analysis of this solution of redissolved crystals, when compared to an original D2E7 sample, showed the same pattern.
  • Concentration values given in the following examples are initial values referring to the antibody solution and the crystallization solution before mixing of the two solutions. All pH values, if not described otherwise, refer to the pH of an acetate buffer stock before it was combined with other substances, like the crystallization agent.
  • All buffer molarities refer to sodium acetate concentrations in a stock solution before pH adjustment, typically performed using acetic acid glacial.
  • D2E7 was brought to a concentration of around 10 mg/mL by diluting the liquid with MiIIi Q water.
  • Batch crystallization was performed by admixing around 500 ⁇ l_ of the protein solution with an equal amount of acetate buffer (0.1 M 1 pH 4.1 or 4.6, respectively) in a well of a 24 well plate. Subsequently, solid sodium dihydrogen phosphate dihydrate was added at six different ratios to each pH setting: around 0.23g, 0.27g, 0.3Og, 0.33g, 0.36g and 0.39g. Thus, after complete dissolution of the crystallization agent, the concentration was around 1.5M to 2.5M in 0.2M steps. The wells were subsequently sealed and the plate was agitated on a laboratory shaker until complete dissolution of the crystallization agent. Thereafter, the 24 well plate was stored at ambient temperature without agitation. Microscopy of the plate was performed after five days.
  • acetate buffer 0.1 M 1 pH 4.1 or 4.6, respectively
  • the acetate buffers were prepared as described in the following: 3 g of acetic acid glacial were diluted with around 42 ml_ of purified water. The pH was ad- justed with sodium hydroxide solution and the volume adjusted to 50 ml_. In this case, the total acetate amount is fixed at 1 M (100 mM in the crystallization solution, or 50 mM in the crystallization mixture) and not expanded by pH adjustment.
  • D2E7 was brought to a concentration of around 10 mg/mL by diluting the liquid with MiIIi Q water.
  • Batch crystallization was performed by admixing around 500 ⁇ l_ of the protein solution with an equal amount of crystallization solution in well of a 24 well plate.
  • 500 ⁇ l_ of a particular crystallization solution was prepared by admixing acetate buffer, sodium di- hydrogen phosphate stock solution, potassium dihydrogen phosphate stock solution and MiIIi Q water in a well.
  • the acetate buffer molarity was 0.1 M
  • the acetate buffer pH was around 4.1 and 4.6, respectively.
  • Sodium dihydrogen phosphate molarity was varied from around 3.4 M to around 4.4 M in 0.2 M steps.
  • the wells were subsequently sealed after preparation of the crystallization mixture to prevent water evaporation. Microscopy of the plate was performed after five days.
  • Crystals as obtained in example 41 are positively charged as determined via zeta potential measurement using a Malvern Instruments Zetasizer nano.
  • an appropriate encapsulating agent is added to the crystal suspension.
  • an appropriate encapsulating agent is a (polymeric) substance with low toxicity, biode- gradability and counter ionic character. Due to this counter ionic character, the substance is attracted to the crystals and allows coating.
  • the crystals are washed and suspended in a buffer containing excipients which conserve crystallinity.
  • the crystals can then be embedded by drying the crystals and combining these dried crystals with a car- rier, e.g. by compression, melt dispersion, etc. encapsulated / embedded by combining a crystal suspension with a carrier solution which is not miscible with water.
  • the carrier precipitates after removal of the solvent of the carrier.
  • the material is dried, encapsulated / embedded by combining a crystal suspension with a water mis- proficient carrier solution.
  • the carrier precipitates as its solubility limit is exceeded in the mixture.
  • embedded by combining dried crystals or a crystal suspension with a water miscible carrier solution.
  • the neutralizing effect of D2E7 solution against the cytotoxic effect of recombinant human TNF (rHuTNF) was determined. This involved incubating mouse L-929 cells as indicator in a 96-well microtiter plate in the presence of various D2E7 concentrations for 48 hours with a defined amount of rHuTNF at 37 0 C. The surviving cells were stained with crystal violet. The intensity of color was measured by spectrophotometry in the individual wells of the microtiter plate and evaluated. The IC 50 was measured, i.e. the concentration of D2E7 which reduced the cytotoxic effect of rHuTNF on L-929 cells such that 50% of the cells survived.
  • the L-929 cell suspension to be used was diluted with medium to provide a concentration of 60,000 cells/mL. Subsequently 100 ⁇ L per well of the respective cell concentration were pipetted into columns 1 -11 of the test plate. The wells in column 12 contained only 100 ⁇ L of medium each. Incubation was applied at 37 0 C and 5% (v/v) CO 2 for 24 hours in the test plate.
  • each of the 9 titer curve dilutions were transferred from the dilution box to the test plate for the reference standard or sample, i.e. for the reference standard to wells in rows A - D in columns 1 - 9 and for the sample to the wells in rows E - H in columns 1 to 9.
  • TNF reference standard (12.5 ng protein/mL medium) were pipetted into the wells in column 1 to 10, row A to H, whereby column 10 corresponded to the 100% lysis value (TNF control).
  • the absorbance of the dye in the test plate wells was measured in a plate photometer at 620 nm. Individual values were plotted on a graph, with the absorbance (y axis) being plotted against the respective dilution or concentration ng/mL (x axis) of antibody. From the 4-parameter plot, the concentration was read off at which half the cells survive and half die (IC 50 value). This concentration was calculated by parameter 3 of the 4-parameter function of the curve data. The mean values of the reference standard concentrations were calculated. The relative biological activity of the sample was calculated by dividing the mean IC 50 value of the reference standard by the individual IC 50 values of the sample and multiplication by 100%. The relative activities were then averaged.
  • the test was performed as a comparison of the biological activity of the sample to that of a reference standard.
  • the absorption values plotted versus the concentration of D2E7 and assessed by a 4-parameter nonlinear regression, revealed the IC 50 values for the inhibition of the TNF effect by the antibody. Since both samples were run in four repeats on one microplate this results in four IC 50 values for D2E7 reference standard and sample respectively.
  • the mean of the IC 50 values of the reference standard was calculated and the relative activity of each repeat of the sample was assessed by dividing the mean IC 50 value of the reference standard by the relevant IC 50 value of the sample and multiplication by 100%.
  • the test of the sample (crystal suspension 2.7 mg/mL, prepared as described in Example 36) revealed a relative biological activity of 111 %.
  • the sample can be considered as fully biologically active.
  • a Nikon Labophot microscope was used, equipped with CFW 10x oculars and 4x, 10x, 2Ox and 4Ox objectives, respectively.
  • Crystal sizes were assessed by transferring the microscopic picture onto a computer screen by means of a JVC TK C1380 color video camera, and by measuring the length or diameter of representative needle-like or needle cluster-like crystals, applying the JVC Digital Screen Measurement Comet software version 3.52a. Furthermore, the mi- croscope was equipped with a filter set (polarizer and analyzer) to assess the birefrin- gent behaviour of samples.
  • birefringence distinguishes ordered crystal- line (anisotropic) from unordered amorphous (isotropic) matter. As birefringence is characteristic for anisotropic matter, this glimmering appearance proves the existence of crystalline matter. However, the absence of birefringence does not exclude the existence of crystalline matter, as the crystals might also exhibit cubic symmetry and therefore be isotropic, like amorphous matter.
  • Figure 1 shows D2E7 crystals obtained by small-scale batch crystallization according to Example 37 after 6 days at room temperature (5 mg/ml final protein concentration; Crystallization buffer: 4.2 M sodium dihydrogen phosphate in 0.1 M sodium acetate, pH 4.1 ). The crystals exhibited birefringence.
  • Figures 2 to 4 show D2E7 crystals obtained by large-scale batch crystallization according to Example 41 b.
  • Syringeability A D2E7 crystal suspension 200 mg/mL protein incorporated in crystals and formulated in a buffer containing 20% (m/v) PEG 4,000 is syringeable through a 27 Vz G needle.
  • Precipitant 4 M NaH 2 PO 4 (dissolved powder in double-distilled water)
  • Method Micro batch crystallization in a hanging-drop tray with 2 ml compartment well, Mixed 500 ⁇ l protein solution with 500 ⁇ l protein; no NaOAc in the solution.
  • Figure 5B The image of Figure 5B (grey) is taken with plane polars and shows the particle morphology.
  • the white crystals on the black background ( Figure 5D) show birefringence and were taken with crossed polars.
  • the blue and orange crystals on the purple background ( Figure 5C) show birefringence and were taken with crossed polar and a red compensator or quarter wave plate.
  • Syringe depletion (1 mL filling volume) was performed as it would be manually by a patient in the course of administration. 20 - 27.5G needle sizes were evaluated.
  • a Dionex HPLC system (P680 pump, ASI 100 autosampler, UVD170U) was used for stability anaysis by SEC.
  • D2E7 samples were separated on a GE Superose ® 6 col- umn, applying a flow rate of 0.5 ml_/min.
  • UV quantitation (detection) was performed at a wavelength of 214 nm.
  • the running buffer consisted of 0.15M sodium chloride in 0.02M sodium phosphate buffer pH 7.5.
  • IR spectra were recorded with a Confocheck system on a Bruker Optics Tensor 27. Liquid samples were analyzed using a MicroBio- lytics AquaSpec cell.
  • compositions comprising crystals of polymeric carrier-stabilized antibodies and fragments for therapeutic uses.
  • PCT Int. Appl. WO. Altus Biologies Inc., USA). 173 pp.

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Abstract

La présente invention concerne un procédé de cristallisation discontinu qui permet de cristalliser un anticorps anti-hTNFalpha, ledit procédé permettant la production dudit anticorps à l'échelle industrielle. L'invention concerne également des cristaux d'anticorps obtenus selon ledit procédé, des compositions contenant lesdits cristaux ainsi que des procédés d'utilisation desdits cristaux et desdites compositions.
PCT/US2007/022622 2006-10-27 2007-10-25 Anticorps anti-htnfalpha cristallisés WO2008057240A2 (fr)

Priority Applications (12)

Application Number Priority Date Filing Date Title
BRPI0717335-0A2A BRPI0717335A2 (pt) 2006-10-27 2007-10-25 Anticorpos anti-htnfalfa cristalinos
NZ576133A NZ576133A (en) 2006-10-27 2007-10-25 Crystalline anti-htnfalpha antibodies
AU2007318120A AU2007318120B2 (en) 2006-10-27 2007-10-25 Crystalline anti-hTNFalpha antibodies
MX2009004351A MX2009004351A (es) 2006-10-27 2007-10-25 Anticuerpos anti-htnfalfa cristalinos.
RU2009119988/10A RU2486296C2 (ru) 2006-10-27 2007-10-25 КРИСТАЛЛИЧЕСКИЕ АНТИТЕЛА ПРОТИВ hTNFα
JP2009534651A JP2010507670A (ja) 2006-10-27 2007-10-25 結晶性抗ｈＴＮＦα抗体
KR1020147033811A KR20150002896A (ko) 2006-10-27 2007-10-25 결정형 항-ｈＴＮＦ알파 항체
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